JP2789436B2 - Garbage incineration agent - Google Patents

Garbage incineration agent

Info

Publication number
JP2789436B2
JP2789436B2 JP4506395A JP4506395A JP2789436B2 JP 2789436 B2 JP2789436 B2 JP 2789436B2 JP 4506395 A JP4506395 A JP 4506395A JP 4506395 A JP4506395 A JP 4506395A JP 2789436 B2 JP2789436 B2 JP 2789436B2
Authority
JP
Japan
Prior art keywords
sludge
product
agent
present
lignin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP4506395A
Other languages
Japanese (ja)
Other versions
JPH08219431A (en
Inventor
真治 浜田
芳樹 因幡
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Seishi KK
Original Assignee
Nippon Seishi KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Seishi KK filed Critical Nippon Seishi KK
Priority to JP4506395A priority Critical patent/JP2789436B2/en
Publication of JPH08219431A publication Critical patent/JPH08219431A/en
Application granted granted Critical
Publication of JP2789436B2 publication Critical patent/JP2789436B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、ゴミ焼却施設に於いて
発生する排ガス中のHCl、SOxを中和除去するのに
有効なゴミ焼却処理剤に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste incineration agent effective for neutralizing and removing HCl and SOx in exhaust gas generated in a waste incineration facility.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】現在、
都市ゴミ清掃工場及び産業廃棄物中間処理工場で稼働し
ている焼却炉では大量に発生している公害の原因となる
塩化水素ガスを石灰或いは苛性ソーダを用いて中和除去
しているのが実状である。この方法には、乾式法、半乾
式法及び湿式法があるが、建設コスト、ランニングコス
ト、その他の諸理由により、主に乾式法と半乾式法が実
施されている。特に、薬剤をスラリーで添加する半乾式
法は中和反応性に優れている方法である。
2. Description of the Related Art
In actual practice, incinerators operating at municipal waste cleaning factories and industrial waste intermediate treatment factories neutralize and remove hydrogen chloride gas, which causes large amounts of pollution, using lime or caustic soda. is there. This method includes a dry method, a semi-dry method, and a wet method, but mainly the dry method and the semi-dry method are implemented due to construction costs, running costs, and other various reasons. In particular, the semi-dry method in which a drug is added as a slurry is a method excellent in neutralization reactivity.

【0003】この場合の薬剤として使用されている石
灰、苛性ソーダにはコストの点で問題があり、その低減
が強く求められているのが現状である。これに対し、生
コンクリート製造工場のミキサ及び生コン運搬車から排
出される残コン及びドラム内の洗浄に伴い発生する生コ
ン残渣を有効利用する方法も提案されているが、セメン
ト分が硬化するため可使日数が制限される欠点がある。
一方、亜硫酸パルプ排液からリグニン製品製造時に副生
産物として発生するスラッジは有効に利用する手段が無
く、埋め立て廃棄処理されている。この産業廃棄物の利
用も課題となっている。
[0003] Lime and caustic soda used as chemicals in this case have a problem in terms of cost, and at present it is strongly required to reduce them. On the other hand, there has been proposed a method of effectively utilizing the remaining concrete discharged from the mixer and ready-mixed concrete truck of the ready-mixed concrete manufacturing plant and the fresh concrete residue generated by washing the inside of the drum. There is a disadvantage that the number of days is limited.
On the other hand, sludge generated as a by-product during the production of lignin products from the sulfite pulp effluent has no means for effectively using it, and is disposed of in landfill. The use of this industrial waste is also an issue.

【0004】[0004]

【課題を解決するための手段】本発明者等は、これ等の
問題を解決するため種々検討した結果、リグニン製品製
造時に副生産物として発生するスラッジが、ゴミ焼却施
設に於いて発生する排ガス中のHCl、SOxを中和除
去するのに有効なゴミ焼却処理剤となりうることを見い
出して本発明に到達したものである。このリグニン製品
製造時に副生産物として発生するスラッジは、炭酸カル
シウム、水酸化カルシウム、炭酸マグネシウム、水酸化
マグネシウムの何れか、若しくはこれ等の混合物が主成
分であり、将に薬剤として適する組成となっている。
The present inventors have conducted various studies to solve these problems, and as a result, sludge generated as a by-product during the production of lignin products has been found to be a waste gas generated in garbage incineration facilities. The present inventors have found that the present invention can be an effective refuse incineration agent for neutralizing and removing HCl and SOx therein, and have reached the present invention. The sludge generated as a by-product during the production of this lignin product is mainly composed of any one of calcium carbonate, calcium hydroxide, magnesium carbonate, and magnesium hydroxide, or a mixture thereof, and has a composition suitable as a drug in general. ing.

【0005】本発明は、 (1)亜硫酸パルプ排液からリグニン製品を製造する
際、副生産物として発生するCa或いはMg系スラッジ
から成るゴミ焼却処理剤、 (2)このゴミ焼却処理剤(1)としてのスラッジが炭
酸カルシウム、水酸化カルシウム、炭酸マグネシウム、
水酸化マグネシウムの何れか、若しくはこれ等の混合物
であるゴミ焼却処理剤、に関するものである。
The present invention, (1) sulphite making the lignin products from the pulp waste solution, a refuse incineration treatment agent consisting of Ca or Mg-based sludge generated as a by-product, (2) the waste incineration agent ( 1) Sludge as calcium carbonate, calcium hydroxide, magnesium carbonate,
Mixture der Lugo Mi incineration agent either, or which like magnesium hydroxide, it relates to.

【0006】本発明に係るゴミ焼却処理剤としてのスラ
ッジは亜硫酸パルプ排液からリグニン製品を製造する
際に副生産物として発生するものである。亜硫酸パルプ
排液には蒸解工程時に使用する薬液によりCa,Na或
いはMgベースがある。これ等の排液に水酸化カルシウ
ム、水酸化マグネシウムを用いて脱糖処理製品を製造す
る際、炭酸カルシウム、炭酸マグネシウム及び未反応の
水酸化カルシウム、水酸化マグネシウムを主成分とする
スラッジが沈殿する。これをセパレータ、デカンタ等の
固液分離装置を用いて本発明に係るゴミ焼却処理剤とし
のスラッジを得るのである。
[0006] The sludge as a refuse incineration agent according to the present invention is generated as a by-product when a lignin product is produced from a sulfite pulp effluent. Sulfite pulp effluents are based on Ca, Na or Mg depending on the chemical used during the cooking step. When producing desalted products using calcium hydroxide and magnesium hydroxide in these effluents, sludge mainly composed of calcium carbonate, magnesium carbonate and unreacted calcium hydroxide and magnesium hydroxide precipitates. . This is used as a garbage incinerator according to the present invention using a solid-liquid separator such as a separator and a decanter.
You get all the sludge.

【0007】このスラッジ中にはリグニン製品が少なか
らず残存している。また、洗浄水も混入している。しか
し、スラッジは貯蔵、運搬及び反応性の点でスラリーで
あることが望ましく、安定なスラリーを得るのにリグニ
ン製品及び洗浄水の混入は反えって好都合である。スラ
ッジスラリーの濃度は貯蔵、運搬及び反応性の点で5〜
90%が望ましい、5%未満では運搬上経済的でなく、
また90%を超えても貯蔵時の取り扱い等が困難とな
る。しかし、粉末製品であれば均一に分散するので使用
することが出来る。
[0007] A considerable amount of lignin product remains in the sludge. Also, washing water is mixed. However, the sludge is desirably a slurry in terms of storage, transportation, and reactivity, and the incorporation of lignin products and washing water is rather advantageous for obtaining a stable slurry. The concentration of sludge slurry is 5 to 5 in terms of storage, transportation and reactivity.
90% is desirable, and less than 5% is not economical for transportation,
Even if it exceeds 90%, handling during storage becomes difficult. However, powder products can be used because they are uniformly dispersed.

【0008】投与量は発生する塩化水素ガス(都市ゴミ
1トン当り塩素ガス約4kg)に対し2倍モル当量以上、
10倍モル当量以下が望ましい。2倍モル当量未満では
中和反応が不充分であり塩化水素ガスが捕集しきれな
い。また、10倍モル当量を超えて添加してもスラッジ
中のリグニン製品がエネルギー源となるメリットはある
ものの、灰分が多くなり焼却灰を増加させることとな
る。焼却炉に投与しても良いし、スラリー中に発生ガス
をトラップする方法を用いても良い。また、生コン残渣
や市販のアルカリ性薬剤と併用することも出来る。
The dose is at least twice the molar equivalent of the generated hydrogen chloride gas (about 4 kg of chlorine gas per ton of municipal waste).
A molar equivalent of 10 times or less is desirable. If it is less than twice the molar equivalent, the neutralization reaction is insufficient and hydrogen chloride gas cannot be collected. Further, even if it is added in excess of 10 times the molar equivalent, the lignin product in the sludge has the merit of being an energy source, but the ash content increases and incineration ash increases. It may be administered to an incinerator or a method of trapping generated gas in slurry may be used. It can also be used in combination with ready-mixed concrete residues or commercially available alkaline chemicals.

【0009】[0009]

【実施例】以下、実施例により本発明を説明する。Ca
ベースのリグニン製品製造時の副生産物を洗浄度を変
え、スラッジ中のリグニン製品量及びスラッジ濃度を変
化させたものを本発明品1,2,3とした。また、Mg
ベースの製品製造時の副生産物を本発明品4とした。本
発明品はそれぞれ表1に示す組成となっている。対照品
には、生コン工場の濃度10%のスラッジスラリーを用
いた。結果を表2に示す。
The present invention will be described below with reference to examples. Ca
The by-products produced during the production of the base lignin product were changed in the degree of washing, and the amounts of the lignin product in the sludge and the sludge concentration were changed to products 1, 2, and 3 of the present invention. In addition, Mg
The by-product at the time of manufacturing the base product was designated as product 4 of the present invention. The products of the present invention have the compositions shown in Table 1, respectively. As a control, a 10% concentration sludge slurry from a ready-mixed concrete factory was used. Table 2 shows the results.

【0010】[0010]

【表1】 [Table 1]

【0011】○燃焼試験 図1の燃焼管式試験装置を用いて、塩化ビニル樹脂のみ
の燃焼試験、塩化ビニル樹脂とスラッジスラリーの混合
物の燃焼試験を行い、発生燃焼ガスの減少率で判定し
た。 図中 1:空気 2:流量計 3:試料 4:ヒータ 5:ポンプ 6:トラップ 7:排気 を示す。減少率が大きいほど中和剤としての効果が優れ
ていることを示す。ガスの定量はJIS K 0102
に準拠した。 試験条件 試料 :塩化ビニル樹脂に中和剤を添加したもの 1
g 燃焼温度:250℃ 燃焼時間:30分 ○安定性試験 中和剤を2週間放置し、1分間撹拌した時の状態を観察
した。沈殿層が固化し撹拌不能の状態を×とした。
Combustion Test Using the combustion tube type test apparatus shown in FIG. 1, a combustion test was conducted on only the vinyl chloride resin and a combustion test was conducted on a mixture of the vinyl chloride resin and the sludge slurry. In the figure, 1: air 2: flow meter 3: sample 4: heater 5: pump 6: trap 7: exhaust. The higher the reduction rate, the better the effect as a neutralizing agent. Quantitative analysis of gas
Compliant. Test conditions Sample: Vinyl chloride resin with neutralizer added 1
g Burning temperature: 250 ° C Burning time: 30 minutes ○ Stability test The neutralizer was left standing for 2 weeks, and the state when stirred for 1 minute was observed. The state where the precipitation layer was solidified and stirring was impossible was evaluated as x.

【0012】[0012]

【表2】 [Table 2]

【0013】[0013]

【発明の効果】本発明品は、ゴミ焼却施設に於いて発生
する排ガス中のHClに対する中和効果及び安定性が、
生コン残渣より優れており、有効なゴミ焼却処理剤とな
りうる。また、リグニン製品製造時に副生するスラッジ
の有効利用が可能となる。
The product of the present invention has a neutralizing effect on HCl in exhaust gas generated in a garbage incineration facility and a stability.
It is superior to ready-mixed concrete residue and can be an effective garbage incineration agent. In addition, sludge produced as a by-product during the production of lignin products can be effectively used.

【図面の簡単な説明】[Brief description of the drawings]

【図1】燃焼管式試験装置の概略を示すフローシートで
ある。
FIG. 1 is a flow sheet schematically showing a combustion tube type test apparatus.

【符号の説明】[Explanation of symbols]

1 空気 2 流量計 3 試料 4 ヒータ 5 ポンプ 6 トラップ 7 排気 1 Air 2 Flow meter 3 Sample 4 Heater 5 Pump 6 Trap 7 Exhaust

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 亜硫酸パルプ排液からリグニン製品を製
造する際に副生産物として発生するCa或いはMg系ス
ラッジから成るゴミ焼却処理剤。
1. A garbage incineration agent comprising Ca or Mg-based sludge generated as a by-product when a lignin product is produced from sulphite pulp effluent.
【請求項2】 スラッジが炭酸カルシウム、水酸化カル
シウム、炭酸マグネシウム、水酸化マグネシウムの何れ
か、若しくはこれ等の混合物である請求項1に記載のゴ
ミ焼却処理剤。
2. The refuse incineration treatment according to claim 1, wherein the sludge is any one of calcium carbonate, calcium hydroxide, magnesium carbonate, and magnesium hydroxide, or a mixture thereof.
JP4506395A 1995-02-10 1995-02-10 Garbage incineration agent Expired - Fee Related JP2789436B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4506395A JP2789436B2 (en) 1995-02-10 1995-02-10 Garbage incineration agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4506395A JP2789436B2 (en) 1995-02-10 1995-02-10 Garbage incineration agent

Publications (2)

Publication Number Publication Date
JPH08219431A JPH08219431A (en) 1996-08-30
JP2789436B2 true JP2789436B2 (en) 1998-08-20

Family

ID=12708904

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4506395A Expired - Fee Related JP2789436B2 (en) 1995-02-10 1995-02-10 Garbage incineration agent

Country Status (1)

Country Link
JP (1) JP2789436B2 (en)

Also Published As

Publication number Publication date
JPH08219431A (en) 1996-08-30

Similar Documents

Publication Publication Date Title
EP0230139B1 (en) Method for cleaning of a hot flue gas stream from waste incineration
EP0364595B1 (en) Method of insolubilizing heavy metals contained in fly ash discharged from garbage incinerator
EP1762309A2 (en) Improvements in and relating to waste processing
US5092931A (en) Method for making insoluble heavy metals contained in fly ash discharged from incinerator
JP2789436B2 (en) Garbage incineration agent
JP2000301103A (en) Detoxification treatment of incineration ash or fly ash
JP2004082100A (en) Method and system for recycling incineration residue
JP2881410B2 (en) Industrial waste treatment method
JPH09187748A (en) Treatment of incineration ash
JP4341001B2 (en) Method for converting organic contaminated soil into cement
JPH09165243A (en) Treatment of waste for cement raw material
JP4834719B2 (en) Waste disposal method
GB2423514A (en) A method of treating waste ash
JPH07239118A (en) Treating method for sludge
JPH10113634A (en) Solidification treatment of flying ashes
JP2003275730A (en) Method for suppressing elution of harmful substance from sewage sludge incineration ash
JPH1163458A (en) Method for processing sludge by incineration
Hjelmar et al. Further development of a process for treatment of APC residues from MSW incinerators
JPS6025581A (en) Disposal of hexavalent chromium-containing coating material
RU2243024C1 (en) Method of treating magnesium production emission gases to remove chlorine and hydrogen chloride
BG65093B1 (en) Method for purifying fume contaminated by hydrogen chloride and heavy metals, rendering said heavy metals inert and turning said hydrogen chloride into a useful product
JP2507858B2 (en) Method for producing organic fertilizer
WO2017194490A1 (en) Process for stabilizing residues resulting from combustion of waste
JP2001146417A (en) Method of producing zeolite
JPH1036118A (en) Production unit for gypsum dihydrate derived from scattered ash

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees